SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2017, Vol. 25 ›› Issue (12): 1863-1870.DOI: 10.1016/j.cjche.2017.04.016

• 第25届中国过程控制会议专栏 • 上一篇    下一篇

Catalytic behavior in propane aromatization using GA-MFI catalyst

Alfredo Aloise, Enrico Catizzone, Massimo Migliori, Jànos B. Nagy, Girolamo Giordano   

  1. University of Calabria, Department of Environmental and Chemical Engineering, Via P. Bucci, I-87036 Rende, CS, Italy
  • 收稿日期:2016-12-23 修回日期:2017-03-01 出版日期:2017-12-28 发布日期:2018-01-18
  • 通讯作者: Massimo Migliori,E-mail address:massimo.migliori@unical.it.

Catalytic behavior in propane aromatization using GA-MFI catalyst

Alfredo Aloise, Enrico Catizzone, Massimo Migliori, Jànos B. Nagy, Girolamo Giordano   

  1. University of Calabria, Department of Environmental and Chemical Engineering, Via P. Bucci, I-87036 Rende, CS, Italy
  • Received:2016-12-23 Revised:2017-03-01 Online:2017-12-28 Published:2018-01-18
  • Contact: Massimo Migliori,E-mail address:massimo.migliori@unical.it.

摘要: Ga-Al-MFI samples were synthesized in hydrothermal conditions from gels of composition 1.08CH3NH2- 0.134TPABr-1SiO2-xAl2O3-yGa2O3-40H2O at 175 ℃ for 7 days, with x = 0.005 and 0.0025, y = 0.005, 0.010 and 0.020. The samples were characterized by XRD, BET measurements, thermal analysis (TGA-DTA) atomic absorption and high resolution solid state MAS 27Al and 71Ga NMRmeasurements. The aromatization of propane was studied as catalytic test. The activity and selectivity of the catalysts were determined for benzene, toluene and xylenes on the one hand and for methane and ethane on the other hand. The most active sample was obtained with the highest Ga/Al ratio. For this sample, the BTX selectivity obtained by aromatizationwas always higher than the hydrocracking selectivity leading tomethane and ethane. The relative amount of toluenewas higher than that of benzene and of xylenes. The samples were deactivated by coke formation thatwas revealedmore severe for the most active sample.

关键词: Propane aromatization, Gallium, ZSM-5, Coke formation, Catalyst deactivation

Abstract: Ga-Al-MFI samples were synthesized in hydrothermal conditions from gels of composition 1.08CH3NH2- 0.134TPABr-1SiO2-xAl2O3-yGa2O3-40H2O at 175 ℃ for 7 days, with x = 0.005 and 0.0025, y = 0.005, 0.010 and 0.020. The samples were characterized by XRD, BET measurements, thermal analysis (TGA-DTA) atomic absorption and high resolution solid state MAS 27Al and 71Ga NMRmeasurements. The aromatization of propane was studied as catalytic test. The activity and selectivity of the catalysts were determined for benzene, toluene and xylenes on the one hand and for methane and ethane on the other hand. The most active sample was obtained with the highest Ga/Al ratio. For this sample, the BTX selectivity obtained by aromatizationwas always higher than the hydrocracking selectivity leading tomethane and ethane. The relative amount of toluenewas higher than that of benzene and of xylenes. The samples were deactivated by coke formation thatwas revealedmore severe for the most active sample.

Key words: Propane aromatization, Gallium, ZSM-5, Coke formation, Catalyst deactivation